Leveling agent, metal plating composition containing same, preparation method therefor and use thereof

ABSTRACT

Disclosed are a leveling agent, a metal plating composition containing same, and a preparation method therefor and the use thereof. The raw materials of the metal electroplating composition comprise a metal plating solution and a leveling agent; the metal plating solution comprises a copper salt, an acidic electrolyte, a source of halide ions and water; and the leveling agent is a compound of formula I. The metal plating composition can be used in the processes of printed circuit board electroplating and integrated circuit copper interconnection electroplating, can achieve the effects of no voids or defects, low purity in the plating layer, good plating homogeneity, a dense structure and small surface roughness, and has better industrial application value.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a 371 National Phase of PCT/CN2017/116441 filed Dec. 15, 2017, which claims the benefit of Chinese Patent Application No. 201710613256.3, filed on Jul. 25, 2017. The entire disclosures of the above applications are incorporated herein by reference.

FIELD OF INVENTION

The present invention relates to the field of semiconductor materials, specifically relates to a leveling agent, metal electroplating composition containing the same, preparation method and uses thereof.

PRIOR ARTS

With the development of Very Large Scale Integration (VLSI) and Ultra Large Scale Integration (ULSI), the integration is increasing and the circuit components are getting denser and denser, chip interconnection becomes a key factor affecting the chip performance. The reliability of the interconnect structures is crucial to the success of VLSI and ULSI and the increase in circuit density. However, due to size limitations of the circuitry, the size reduction of interconnects in VLSI and ULSI technologies has raised additional demands on the processing capacity, which comprise the precise processing of multilayer, high aspect ratio structural features.

The width, aperture size, and other feature size of the interconnect decrease with the increase of circuit density. However, the thickness of the dielectric layer will not decrease proportionally. As a result, the aspect ratio feature increases. Secondly, in the back end of line process of integrated circuits, copper has gradually replaced aluminum as the predominant material used in interconnect technology of VLSI interconnection. In current chip manufacturing, the wiring and interconnection of the chip are almost entirely copper plated.

Copper has a lower resistivity (about 35% lower) and a higher resistance to electromigration (about twice as aluminum) than aluminum. Moreover, copper has good thermal conductivity, which is advantageous to the devices of multilayer integration with higher circuit density and current density. Copper can be coated on the substrate by electroplating, sputtering, physical vapor deposition, and chemical vapor deposition. The damascene process (Damascus process) in the form of electroplating is generally considered to be the best method for preparing copper interconnects. The copper damascene process can be filled with micronanoscale pores by electroplating, which has the characteristics of high deposition speed and low cost.

However, with the continuous development of the integrated circuit technology, the requirements for filling the pores of nanoscale are becoming more stringent. Researchers from all over the world are eager to study electroplating methods, electroplating solutions and additives for printed circuit board plating and integrated circuit copper interconnect plating processes to achieve the effects that no hole or defect exists between the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure, and small surface roughness.

Generally, the leveling agents for copper plating can better level the sediment across the surface of the substrate, but tend to impair the uniform-plating capacity of the plating bath. The uniform-plating capacity is defined as the ratio of the thickness of the copper sediment in the center of the pore to the thickness at its surface.

Patent Application No. CN105683250A has disclosed a polymer leveling agent comprising an imidazole structure, which can be used to solve the problem of uniform-plating on PCB plating. However, it is not effective in the application of nano scale Damascus copper interconnect plating.

Therefore, there is an urgent need in the art to develop electroplating methods, electroplating solutions and additives used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which achieve the effects that no hole or defect between the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure, and small surface roughness.

CONTENT OF THE PRESENT INVENTION

An object of the present invention is to provide a leveling agent, metal electroplating composition containing the same, preparation method and uses thereof, in order to solve the problem that the metal plating layers made by the prior electroplating method, electroplating solution and additives have holes and defects, high plating layer impurity, poor uniform-plating property, poor structure density, and rough surface. The leveling agent and the metal electroplating composition containing the leveling agent can be used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which can achieve the effects of no hole or defect in the metal plating layers, low plating layer impurity, good uniform-plating property, compact structure and small surface roughness, and has better industrial application value.

The present invention solves the above technical problems by the following technical solutions.

The first aspect of the present invention provides a use of the compound of formula I as a leveling agent in metal electroplating composition

wherein,

R₁ is C₁-C₅ alkyl, propargyl, allyl or benzyl;

R₂ is H, C₁-C₅ alkyl, hydroxy-substituted C₁-C₅ alkyl, unsaturated five-membered heterocyclic substituted C₁-C₃ alkyl, phenyl, halogenated phenyl, benzyl, halogenated benzyl or a hydroxyl-substituted benzyl;

R₃ is substituted or unsubstituted phenyl, pyridyl, naphthyl, hydroxy-substituted naphthyl, thienyl, furyl or indolyl;

R₄ is H or C₁-C₅ alkyl;

The substituent of the substituted phenyl is selected from the group consisting of halogen, C₁-C₅ alkyl, nitro, methoxy, hydroxy and C₁-C₃ alkylamino; the substituents are the same or different when there are more than one substituents attached;

the heteroatom in the unsaturated five-membered heterocyclic ring is selected from the group consisting of O, N and S, and the number of heteroatoms is 1 to 3, the heteroatoms are the same or different when there are more than one heteroatoms.

In the use,

preferably, R₁ is methyl, propyl, benzyl, propargyl or allyl;

preferably, R₂ is benzyl, methyl, hydroxyethyl, thiophene-substituted methyl, furan-substituted ethyl, monohalogenated benzyl (such as

or hydroxy-substituted benzyl (such as

preferably, R₃ is pyridyl (such as

thienyl (such as

indolyl (such as

naphthyl (such as

hydroxy-substituted naphthyl (such as

phenyl, hydroxy-substituted phenyl (such as

monohalogenated phenyl (such as

methylphenyl (such as

nitrophenyl (such as

methoxyphenyl (such as

or dimethylamino-substituted phenyl (such as

preferably, R₄ is H or methyl;

the use, wherein,

the leveling agent is preferably selected from the group consisting of:

Compound 1: R₁=Propyl-; R₂=Bn-; R₃=Ph-; R₄═H—;

Compound 2: R₁=Propyl-; R₂=Bn-; R₃=2-Cl-Ph-; R₄═H—;

Compound 3: R₁=Propyl-; R₂=Bn-; R₃=3-Cl-Ph-; R₄═H—;

Compound 4: R₁=Propyl-; R₂=Bn-; R₃=4-Cl-Ph-; R₄═H—;

Compound 5: R₁=Propyl-; R₂=Bn-; R₃=4-Br-Ph-; R₄═H—;

Compound 6: R₁=Propyl-; R₂=Bn-; R₃=2-F-Ph-; R₄═H—;

Compound 7: R₁=Propyl-; R₂=Bn-; R₃=4-Me-Ph-; R₄═H—;

Compound 8: R₁=Propyl-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—;

Compound 9: R₁=Propyl-; R₂=Bn-; R₃=4-NO₂-Ph-; R₄═H—;

Compound 10: R₁=Propyl-; R₂=Bn-; R₃=4-(N,N—(CH₃)₂)-Ph-; R₄═H—;

Compound 11: R₁=Propyl-; R₂=Bn-;

R₄═H—;

Compound 12: R₁=Propyl-; R₂=Bn-;

R₄═H—;

Compound 13: R₁=Propyl-; R₂=Bn-;

R₄═H—;

Compound 14: R₁=Propyl-; R₂=Bn-;

R₄═H—;

Compound 15: R₁=Propyl-; R₂=Bn-;

R₄═H—;

Compound 16: R₁=Propyl-; R₂=Bn-; R₃=Ph-; R₄═CH₃—;

Compound 17: R₁=Propyl-; R₂=Bn-; R₃=4-MeO-Ph-; R₄═CH₃—;

Compound 18: R₁=Propyl-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 19: R₁=Propyl-; R₂=Bn-; R₃=4-OH-Ph-; R₄═CH₃—;

Compound 20: R₁=Propyl-; R₂=Bn-; R₃=4-Br-Ph-; R₄═CH₃—;

Compound 21: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—;

Compound 22: R₁=Propyl-; R₂=2-Cl-Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 23: R₁=Propyl-; R₂=3-Cl-Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 24: R₁=Propyl-; R₂=4-Cl-Bn-; R₃=2-OH-Ph-; R₄—CH₃—;

Compound 25: R₁=Propyl-; R₂=4-Br-Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 26: R₁=Propyl-; R₂=4-F-Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 27: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—;

Compound 28: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—;

Compound 29: R₁=Propyl-; R₂=4-OH-Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 30: R₁=Propargyl-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—;

Compound 31: R₁=Propargyl-; R₂=Bn-;

R₄═H—;

Compound 32: R₁=Propargyl-; R₂=Bn-; R₃=4-(N,N—(CH₃)₂)-Ph-; R₄═H—;

Compound 33: R₁=Propargyl-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—;

Compound 34: R₁=Bn-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—; and

Compound 35: R₁=Bn-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—.

In the present invention, the compound represented by formula I is prepared in accordance with the method disclosed in Chinese Patent Application CN201610853873.6.

The second aspect of the present invention provides a metal electroplating composition, wherein the raw material of the metal electroplating composition comprises a metal electroplating liquid and the leveling agent as defined in the first aspect of the present invention; the metal electroplating liquid comprises a copper salt, acidic electrolyte, halide ions source and water.

The metal electroplating composition, wherein,

The copper salt is preferably selected from the group consisting of copper sulfate, copper halide, copper acetate, copper nitrate, copper fluoroborate, copper alkylsulfonate, copper aryl sulfonate, copper sulfamate and copper gluconate; the copper alkylsulfonate is preferably selected from the group consisting of copper methanesulfonate, copper ethanesulfonate and copper propanesulfonate; the copper aryl sulfonate is preferably selected from the group consisting of copper phenyl sulfonate, copper phenolsulfonate and copper p-toluenesulfonate. The molar concentration of the copper ions in the metal electroplating liquid is 0.15-2.85 mol/L.

The acidic electrolyte is preferably selected from the group consisting of sulfuric acid, phosphoric acid, acetic acid, fluoroboric acid, sulfamic acid, alkyl sulfonic acid, aryl sulfonic acid and hydrochloric acid. The alkyl sulfonic acid is preferably selected from the group consisting of methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid and trifluoromethanesulfonic acid; the aryl sulfonic acid is preferably selected from the group consisting of phenylsulfonic acid, phenolsulfonic acid and toluenesulfonic acid. In each liter of the metal electroplating composition, the mass of the acidic electrolyte is preferably 1-300 g.

The halide ions source is preferably a chloride ions source. The chloride ions source is preferably selected from the group consisting of copper chloride, tin chloride and hydrochloric acid. The concentration of the halide ions of the halide ions source is preferably 0-100 ppm but not 0, more preferably 50-100 ppm.

In the present invention, the metal electroplating liquid is preferably an electroplating copper solution SYS^(D)2110, and the manufacturer thereof is Shanghai Xinyang Semiconductor Material Co., Ltd. The preparation of SYS^(D)2110 can refer to the method disclosed in Chinese Patent No. CN100529194C.

In the present invention, the raw material of the metal electroplating composition further comprises an accelerator, wherein the accelerator (also referred to as a brightener) refers to an organic additive capable of increasing the plating rate of the plating bath, and the accelerator is the accelerator acceptable in the art. The accelerator is preferably selected from the group consisting of N,N-dimethyl-disulfenyl carbamic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonic acid-(3-sulfopropyl) ester, 3-mercapto-propyl sulfonate sodium salt; disulfenyl carbonate-o-ethyl ester-s-ester and 3-mercapto-1-propane sulfonate potassium salt, disulfopropyl disulfide, 3-(benzothiazolyl-s-sulfenyl)propyl sulfonate sodium salt, pyridinium propyl sulfonyl betaine, 1-sodium-3-mercapto propane-1-sulfonate, N,N-dimethyl-disulfenyl carbamic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl propyl sulfonic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl sulfonate sodium salt, carbonic acid-disulfenyl-o-ethyl ester-s-ester and 3-mercapto-1-ethanesulfonate potassium salt, disulfoethyl disulfide, 3-(benzothiazolyl-s-sulfenyl)ethyl sulfonate sodium salt, pyridinium ethyl sulfonyl betaine and 1-sodium-3-mercaptoethane-1-sulfonate; the concentration of the accelerator is preferably 0.1 ppm-1000 ppm.

In a preferred embodiment of the present invention, the accelerator is UPD3115A, which is applied by Shanghai Xinyang Semiconductor Materials Co., Ltd.

In the present invention, the raw material of the metal electroplating composition further comprises an inhibitor, and the inhibitor refers to an organic additive capable of suppressing the rate of metal electroplating. The inhibitor is preferably selected from the group consisting of polypropylene glycol copolymer, polyethylene glycol copolymer, ethylene oxide-propylene oxide (EO/PO) copolymer and butanol-ethylene oxide-propylene oxide copolymer; the butanol-ethylene oxide-propylene oxide copolymer preferably has a weight-average molecular weight of 100-100,000, more preferably 500-10,000; the concentration of the inhibitor is preferably 1-10000 ppm, more preferably 5-10000 ppm.

In a preferred embodiment of the invention, the inhibitor is UPD3115S, which is applied by Shanghai Xinyang Semiconductor Materials Co., Ltd.

In the present invention, the concentration of the leveling agent is the concentration acceptable in the art, preferably 1-10 ppm, more preferably 5-10 ppm.

In a preferred embodiment of the invention, the raw material of the metal electroplating composition consists of the metal electroplating liquid, the leveling agent, the accelerator and the inhibitor.

The third aspect of the present invention provides a method for preparing the metal electroplating composition as defined in the second aspect of the present invention, which preferably comprises mixing the raw material components uniformly.

The fourth aspect of the present invention provides the use of the metal electroplating composition as defined in the second aspect of the present invention in printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, the use preferably comprises:

(1) contacting the substrate to be electroplated with the metal electroplating composition;

(2) applying an electric current for electroplating.

In step (1), the substrate is any substrate acceptable in the art, preferably a wafer or chip of a printed circuit board or an integrated circuit.

In step (2), the current density of the electroplating is acceptable in the art, preferably 0.1-10 ASD, more preferably 0.3-5 ASD, the most preferably 0.5-1.5 ASD;

in step (2), the electroplating time is acceptable in the art, preferably 53-110 s, preferably 80-110 s.

in step (2), the electroplating temperature is acceptable in the art, preferably 10-65° C., more preferably 10-35° C., the most preferably 20-30° C.

In a preferred embodiment of the invention, step (2) is preferably carried out in three steps:

in the first step, the current density is 0.1-0.5 ASD, more preferably 0.3 ASD; the electroplating time is 3-20 s, more preferably 10 s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.;

in the second step, the current density is 0.5-1.5 ASD, more preferably 1.0 ASD; the electroplating time is 20-30s, more preferably 25s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.;

in the third step, the current density is 1-10 ASD, more preferably 5 ASD; the electroplating time is 30-60s, more preferably 45s; the electroplating temperature is 10-65° C., more preferably 10-35° C., the most preferably 20-30° C., for example 25° C.

In the present invention, the term “Propyl-” refers to propyl, of which structure is

In the present invention, the term “Propargyl-” refers to propargyl, of which structure is

In the present invention, the term “Bn-” refers to benzyl, of which structure is

In the present invention, the term “Ph-” refers to phenyl, of which structure is

In the present invention, the term “C₁-C₅ alkyl” is preferably methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl or neopentyl. Unless otherwise specified, propyl, butyl or pentyl refers to n-propyl, n-butyl or n-pentyl, respectively.

In the present invention, the term “unsaturated five-membered heterocyclic ring” preferably has aromaticity. The unsaturated five-membered heterocyclic ring is preferably furan, thiophene, pyrazole, imidazole, thiazole, triazole or tetrazolium and the like.

In the present invention, the term “hydroxy-substituted X group” refers to an X group substituted by one or more than one hydroxy (the number of hydroxy depends on the number of H atoms, for example 1-6, preferably 1-3), wherein the position of the hydroxy is optional. For example, “hydroxy substituted benzyl” refers to a benzyl group substituted with one or more hydroxy, including but not limited to

and the like.

In the present invention, the term “halogenated Y group” refers to a Y group substituted by one or more than one halogens (the number of halogens may be determined according to the number of H, for example 1 to 6, preferably 1 to 3). For example, halogenated phenyl refers to a phenyl substituted with one or more than one halogens, wherein the halogens may be the same or different, including but not limited to

and the like.

In the present invention, the term “halogen” refers to F, Cl, Br or I.

In the present invention, the term “concentration” refers to the concentration of each substance in 1 L metal electroplating liquid.

In the present invention, unless otherwise specified in the context, the following abbreviations should have the following meanings: A=amperes; A/dm2=amps per square decimeter=ASD; ° C.=degrees Celsius; ppm=parts per million. Unless otherwise indicated, all % refer to mass percentage. All numerical ranges are inclusive and can be combined in any order, but it is obvious that the sum of such numerical ranges are limited to 100%.

In the present invention, “feature” refers to the geometry on the substrate. “Aperture” refers to a sunken feature that comprises a through hole and a blind channel. “Halide” refers to fluoride, chloride, bromide and iodide.

In the present invention, the temperature of “ice bath” refers to −5° C.−5° C., preferably −5° C.−0° C.

Based on the common knowledge in the art, the above various preferred conditions can be optionally combined to obtain preferred embodiments of the present invention.

The reagents and raw materials used in the present invention are commercially available.

The positive effects of the present invention are as follows:

the metal electroplating composition of the present invention comprises a leveling agent represented by the formula I. The metal electroplating composition can be used for printed circuit board electroplating and integrated circuit copper interconnection electroplating processes, which achieves the effects of free of holes and defects, low plated layer impurity, good uniform-plating property, compact structure, and small surface roughness. Furthermore, the metal electroplating composition has good thermal reliability and uniform-plating property, and can solve the problem of orifice sealing, and has good industrial application value.

EMBODIMENT Preparation Embodiments: Preparation of Metal Electroplating Compositions 1-35 and Comparative Metal Electroplating Compositions 1-6

The components of the metal electroplating compositions 1-35 and the comparative metal electroplating compositions 1-6 are shown in Table 1, wherein, the metal ions source and the electrolyte is provided by electroplating copper solution of the trademark SYS^(D)2110, which is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd. The accelerator of the trademark UPD3115 A is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd. The inhibitor of the trademark UPD3115S is purchased from Shanghai Xinyang Semiconductor Materials Co., Ltd.

TABLE 1 Amount Electro- of Amount plating electroplating Amount Amount of Formula copper Leveling copper of of leveling No. solution Accelerator Inhibitor agent solution accelerator inhibitor agent Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 1 L 10 ppm 100 ppm 1 ppm electroplating composition 1 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 2 1 L 50 ppm 500 ppm 5 ppm electroplaing composition 2 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 3 1 L 100 ppm  1000 ppm  10 ppm  electroplating composition 3 Metal SYS^(D)2110 N,N- Butanol- Compound 4 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene composition 4 disulfenyl oxide- carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 5 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene composition 5 propane-1- oxide- sulfonate alkylene oxide, Mw = 3000 Metal SYS^(D)2110 3- Butanol- Compound 6 1 L 100 ppm  1000 ppm  10 ppm  electroplating (benzothiazolyl- ethylene composition 6 s- oxide- sulfenyl)propyl alkylene sulfonate oxide, sodium salt Mw = 10000 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 7 1 L 10 ppm 100 ppm 1 ppm electroplating composition 7 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 8 1 L 50 ppm 500 ppm 5 ppm electroplating composition 8 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 9 1 L 100 ppm  1000 ppm  10 ppm  electroplating composition 9 Metal SYS^(D)2110 N,N- Butanol- Compound 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene 10 composition disulfenyl oxide- 10 carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene 11 composition propane-1- oxide- 11 sulfonate alkylene oxide, Mw = 3000 Metal SYS^(D)2110 3- Butanol- Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating (benzothiazolyl- ethylene 12 composition s- oxide- 12 sulfenyl)propyl alkylene sulfonate oxide, sodium salt Mw = 10000 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 10 ppm 100 ppm 1 ppm electroplating 13 composition 13 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 50 ppm 500 ppm 5 ppm electroplating 14 composition 14 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating 15 composition 15 Metal SYS^(D)2110 N,N- Butanol- Compound 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene 16 composition disulfenyl oxide- 16 carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene 17 composition propane-1- oxide- 17 sulfonate alkylene oxide, Mw = 3000 Metal SYS^(D)2110 3- Butanol- Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating (benzothiazolyl- ethylene 18 composition s- oxide- 18 sulfenyl)propyl alkylene sulfonate oxide, sodium salt Mw = 10000 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 10 ppm 100 ppm 1 ppm electroplating 19 composition 19 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 50 ppm 500 ppm 5 ppm electroplating 20 composition 20 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating 21 composition 21 Metal SYS^(D)2110 N,N- Butanol- Compound 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene 22 composition disulfenyl oxide- 22 carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene 23 composition propane-1- oxide- 23 sulfonate alkylene oxide, Mw = 3000 Metal SYS^(D)2110 3- Butanol- Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating (benzothiazolyl- ethylene 24 composition s- oxide- 24 sulfenyl)propyl alkylene sulfonate oxide, sodium salt Mw = 10000 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 10 ppm 100 ppm 1 ppm electroplating 25 composition 25 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 50 ppm 500 ppm 5 ppm electroplating 26 composition 26 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating 27 composition 27 Metal SYS^(D)2110 N,N- Butanol- Compound 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene 28 composition disulfenyl oxide- 28 carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene 29 composition propane-1- oxide- 29 sulfonate alkylene oxide, Mw = 3000 Metal SYS^(D)2110 3- Butanol- Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating (benzothiazolyl- ethylene 30 composition s- oxide- 30 sulfenyl)propyl alkylene sulfonate oxide, sodium salt Mw = 10000 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 10 ppm 100 ppm 1 ppm electroplating 31 composition 31 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 50 ppm 500 ppm 5 ppm electroplating 32 composition 32 Metal SYS^(D)2110 UPD3115 A UPD3115S Compound 1 L 100 ppm  1000 ppm  10 ppm  electroplating 33 composition 33 Metal SYS^(D)2110 N,N- Butanol- Compound 1 L 10 ppm 100 ppm 1 ppm electroplating dimethyl- ethylene 34 composition disulfenyl oxide- 34 carbamic alkylene acid-(3- oxide, sulfopropyl)ester Mw = 1000 Metal SYS^(D)2110 1-sodium-3- Butanol- Compound 1 L 50 ppm 500 ppm 5 ppm electroplating mercapto ethylene 35 composition propane-1- oxide- 35 sulfonate alkylene oxide, Mw = 3000 Comparative SYS^(D)2110 UPD3115 A UPD3115S The 1 L 10 ppm 100 ppm 1 ppm Metal polymer electroplating obtained composition 1 by the method of Example 1 in CN105705491 A Comparative SYS^(D)2110 UPD3115 A UPD3115S The 1 L 50 ppm 500 ppm 5 ppm Metal polymer electroplating obtained composition 2 by the method of Example 2 in CN105705491 A Comparative SYS^(D)2110 UPD3115 A UPD3115S The 1 L 100 ppm  1000 ppm  10 ppm  Metal polymer electroplating obtained composition 3 by the method of Example 3 in CN105705491 A Comparative SYS^(D)2110 N,N- Butanol- The 1 L 10 ppm 100 ppm 1 ppm Metal dimethyl- ethylene polymer electroplating disulfenyl oxide- obtained composition 4 carbamic alkylene by the acid-(3- oxide, method of sulfopropyl)ester Mw = 1000 Example 1 in CN105705491 A Comparative SYS^(D)2110 1-sodium-3- Butanol- The 1 L 50 ppm 500 ppm 5 ppm Metal mercapto ethylene polymer electroplating propane-1- oxide- obtained composition 5 sulfonate alkylene by the oxide, method of Mw = 3000 Example 2 in CN105705491 A Comparative SYS^(D)2110 3- Butanol- The 1 L 100 ppm  1000 ppm  10 ppm  Metal (benzothiazolyl- ethylene polymer electroplating s- oxide- obtained composition 6 sulfenyl)propyl alkylene by the sulfonate oxide, method of sodium salt Mw = 10000 Example 3 in CN105705491 A

Application Embodiments 1-35 and Comparative Application Embodiments 1-6

In the present invention, Application embodiments 1-35 and Comparative application embodiments 1-6 are carried out with metal electroplating compositions 1-35 and comparative metal electroplating compositions 1-6, respectively. The parameters of the electroplating process are carried out according to the parameters listed in Table 2.

TABLE 2 Pattern wafer with PVD seed layer (graphics) Electroplating Current Electroplating Electroplating Electroplating target parameters density time temperature Embodiment Three-step Step 1 0.1  3 s 20° C. 1, 4, 7, 10, electroplating ASD 13, 16, 19, Step 2 0.5 20 s 20° C. 22, 25, 28, ASD 31, 34 Step 3  1 ASD 30 s 20° C. Embodiment Three-step Step 1 0.3 10 s 25° C. 2, 5, 8, 11, electroplating ASD 14, 17, 20, Step 2 1.0 25 s 25° C. 23, 26, 29, ASD 32, 35 Step 3  5 ASD 45 s 25° C. Embodiment Three-step Step 1 0.5 20 s 30° C. 3, 6, 9, 12, electroplating ASD 15, 18, 21, Step 2 1.5 30 s 30° C. 24, 27, 30, ASD 33 Step 3 10 ASD 60 s 30° C. Comparative Three-step Step 1 0.1  3 s 20° C. Application electroplating ASD Embodiment 1 Step 2 0.5 20 s 20° C. ASD Step 3  1 ASD 30 s 20° C. Comparative Three-step Step 1 0.3 10 s 25° C. Application electroplating ASD Embodiment 2 Step 2 1.0 25 s 25° C. ASD Step 3  5 ASD 45 s 25° C. Comparative Three-step Step 1 0.5 20 s 30° C. Application electroplating ASD Embodiment Step 2 1.5 30 s 30° C. 3 ASD Step 3 10 ASD 60 s 30° C. Comparative Three-step Step 1 0.1  3 s 20° C. Application electroplating ASD Embodiment 4 Step 2 0.5 20 s 20° C. ASD Step 3  1 ASD 30 s 20° C. Comparative Three-step Step 1 0.3 10 s 25° C. Application electroplating ASD Embodiment Step 2 1.0 25 s 25° C. 5 ASD Step 3  5 ASD 45 s 25° C. Comparative Three-step Step 1 0.5 20 s 30° C. Application electroplating ASD Embodiment Step 2 1.5 30 s 30° C. 6 ASD Step 3 10 ASD 60 s 30° C.

Application Effects

The application effect is shown in Table 3. Wherein, the impurity content is analyzed by elemental analysis of combustion method, and the holes condition, the uniform-plating property, the structure compactness and the surface roughness are observed by SEM electron microscopy.

TABLE 3 Impurity Impurity Impurity in in in plated plated plated uniform- Holes layer layer layer plating Structure Surface No. condition (C) (O) (S) property compactness roughness Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 1 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 2 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 3 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 4 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 5 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 6 orifice bulge Application Small <20 ppm <10 ppm <10 ppm Slight Slightly Slightly embodiment 7 holes orifice loose rough bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 8 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment 9 orifice bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 10 bulge Application Small <20 ppm <10 ppm <10 ppm Slight Slightly Slightly embodiment holes or orifice loose rough 11 defects bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 12 bulge Application No hole <20 ppm <10 ppm <10 ppm No orifice compact Smooth embodiment orifice 13 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 14 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 15 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 16 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 17 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 18 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 19 bulge Application Small <20 ppm <10 ppm <10 ppm Slight Slightly Slightly embodiment holes orifice loose rough 20 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 21 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 22 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 23 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 24 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 25 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 26 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 27 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 28 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 29 bulge Application Small <20 ppm <10 ppm <10 ppm Slight Slightly Slightly embodiment holes orifice loose rough 30 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 31 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 32 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 33 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 34 bulge Application No hole <20 ppm <10 ppm <10 ppm No compact Smooth embodiment orifice 35 bulge Comparative Large >20 ppm >10 ppm >10 ppm Obvious Loose Rough application holes orifice embodiment 1 bulge Comparative Only a >20 ppm >10 ppm >10 ppm more Loose Rough application few orifice embodiment 2 holes bulge Comparative Only a >20 ppm >10 ppm >10 ppm more Loose Slightly application few orifice rough embodiment 3 holes bulge Comparative Large >20 ppm >10 ppm >10 ppm Obvious Loose Rough application holes orifice embodiment 4 bulge Comparative Only a >20 ppm >10 ppm >10 ppm more Loose Rough application few orifice embodiment 5 holes bulge Comparative Only a >20 ppm >10 ppm >10 ppm more Loose Slightly application few orifice rough embodiment 6 holes bulge

The above embodiments show that using the metal electroplating compositions of the present invention for electroplating can achieve the effects of free of hole or defect, low plating layer impurity, good uniform-plating property, compact structure, and low surface roughness. Meanwhile, the usage of the polymer leveling agent containing imidazole structure disclosed in Patent application No. CN105705491A has the disadvantages of free of holes and defects, high plating layer impurity, poor uniform-plating property, loose structure, high surface roughness.

Although the specific embodiments of the present invention are described above, a person skilled in the art should understand that these are only examples and can be changed or modified in a variety of ways without deviating from the principle and essence of the present invention. Accordingly, the scope of the present invention is defined by the appended claims. 

What is claimed is:
 1. A metal electroplating composition, wherein a raw material of the metal electroplating composition comprises a leveling agent represented by formula I,

wherein, R₁ is C₁-C₅ alkyl, propargyl, allyl or benzyl; R₂ is H, C₁-C₅ alkyl, hydroxy-substituted C₁-C₅ alkyl, unsaturated five-membered C₁-C₃ alkyl substituted by an unsaturated five-membered heterocycle, phenyl, halogenated phenyl, benzyl, halogenated benzyl, or a hydroxyl-substituted benzyl; R₃ is substituted or unsubstituted phenyl, pyridyl, naphthyl, hydroxy-substituted naphthyl, thienyl, furyl or indolyl; R₄ is H or C₁-C₅ alkyl; the substituted phenyl includes at least one substituent that is selected from the group consisting of halogen, C₁-C₅ alkyl, nitro, methoxy, hydroxy and C₁-C₃ alkylamino, and when the substituted phenyl includes more than one substituent each of the substituents are the same or different; a heteroatom in the unsaturated five-membered heterocyclic ring is selected from the group consisting of O, N and S, and the number of heteroatoms is 1 to 3, and the heteroatoms are the same or different when there are more than one heteroatoms, wherein the raw material of the metal electroplating composition comprises a metal electroplating liquid; and the metal electroplating liquid comprises a copper salt, an acidic electrolyte, a halide ion source, and water.
 2. The metal electroplating composition according to claim 1, wherein in the leveling agent represented by formula I, at least one of the following is present: R₁ is methyl, propyl, benzyl, propargyl or allyl; R₂ is benzyl, methyl, hydroxyethyl, thiophene-substituted methyl, furan-substituted ethyl, monohalogenated benzyl, or hydroxy-substituted benzyl; R₃ is pyridyl, thienyl, indolyl, naphthyl, hydroxy-substituted naphthyl, phenyl, hydroxy-substituted phenyl, monohalogenated phenyl, methylphenyl, nitrophenyl, methoxyphenyl or dimethylamino phenyl; R₄ is H or methyl; and the halogen is F, Cl or Br.
 3. The metal electroplating composition according to claim 1, wherein the leveling agent represented by formula I is selected from the group consisting of Compound 1: R₁=Propyl-; R₂=Bn-; R₃=Ph-; R₄═H—; Compound 2: R₁=Propyl-; R₂=Bn-; R₃=2-Cl-Ph-; R₄═H—; Compound 3: R₁=Propyl-; R₂=Bn-; R₃=3-Cl-Ph-; R₄═H—; Compound 4: R₁=Propyl-; R₂=Bn-; R₃=4-Cl-Ph-; R₄═H—; Compound 5: R₁=Propyl-; R₂=Bn-; R₃=4-Br-Ph-; R₄═H—; Compound 6: R₁=Propyl-; R₂=Bn-; R₃=2-F-Ph-; R₄═H—; Compound 7: R₁=Propyl-; R₂=Bn-; R₃=4-Me-Ph-; R₄═H—; Compound 8: R₁=Propyl-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—; Compound 9: R₁=Propyl-; R₂=Bn-; R₃=4-NO₂-Ph-; R₄═H—; Compound 10: R₁=Propyl-; R₂=Bn-; R₃=4-(N,N—(CH₃)₂)-Ph-; R₄═H—; Compound 11: R₁=Propyl-; R₂=Bn-;

R₄═H—; Compound 12: R₁=Propyl-; R₂=Bn-;

R₄═H—; Compound 13: R₁=Propyl-; R₂=Bn-;

R₄═H—; Compound 14: R₁=Propyl-; R₂=Bn-;

R₄═H—; Compound 15: R₁=Propyl-; R₂=Bn-;

R₄═H—; Compound 16: R₁=Propyl-; R₂=Bn-; R₃=Ph-; R₄═CH₃—; Compound 17: R₁=Propyl-; R₂=Bn-; R₃=4-MeO-Ph-; R₄═CH₃—; Compound 18: R₁=Propyl-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 19: R₁=Propyl-; R₂=Bn-; R₃=4-OH-Ph-; R₄═CH₃—; Compound 20: R₁=Propyl-; R₂=Bn-; R₃=4-Br-Ph-; R₄═CH₃—; Compound 21: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—; Compound 22: R₁=Propyl-; R₂=2-Cl-Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 23: R₁=Propyl-; R₂=3-Cl-Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 24: R₁=Propyl-; R₂=4-Cl-Bn-; R₃=2-OH-Ph-; R₄—CH₃—; Compound 25: R₁=Propyl-; R₂=4-Br-Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 26: R₁=Propyl-; R₂=4-F-Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 27: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—; Compound 28: R₁=Propyl-;

R₃=2-OH-Ph-; R₄═CH₃—; Compound 29: R₁=Propyl-; R₂=4-OH-Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 30: R₁=Propargyl-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—; Compound 31: R₁=Propargyl-; R₂=Bn-;

R₄═H—; Compound 32: R₁=Propargyl-; R₂=Bn-; R₃=4-(N,N—(CH₃)₂)-Ph-; R₄═H—; Compound 33: R₁=Propargyl-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—; Compound 34: R₁=Bn-; R₂=Bn-; R₃=3,4,5-(MeO)₃-Ph-; R₄═H—; and Compound 35: R₁=Bn-; R₂=Bn-; R₃=2-OH-Ph-; R₄═CH₃—.
 4. The metal electroplating composition according to claim 1, wherein the metal electroplating liquid includes at least one selected from the group consisting of: the copper salt being selected from the group consisting of copper sulfate, copper halide, copper acetate, copper nitrate, copper fluoroborate, copper alkylsulfonate, copper arylsulfonate, copper sulfamate and copper gluconate; a molar concentration of copper ions in the metal electroplating liquid being in a range of 0.15-2.85 mol/L; the acidic electrolyte being selected from the group consisting of sulfuric acid, phosphoric acid, acetic acid, fluoroboric acid, sulfamic acid, alkylsulfonic acid, arylsulfonic acid and hydrochloric acid; in each liter of the metal electroplating composition, a mass of the acidic electrolyte being 1-300 g; the halide ion source being a chloride ion source; a concentration of the halide ion of the halide ion source being 0-100 ppm; and a concentration of the leveling agent being 1-10 ppm.
 5. The metal electroplating composition according to claim 4, wherein, the metal electroplating liquid includes at least one selected from the group consisting of: the copper alkylsulfonate being selected from the group consisting of copper methanesulfonate, copper ethanesulfonate and copper propanesulfonate; the copper arylsulfonate being selected from the group consisting of copper phenyl sultanate, copper phenolsulfonate and copper p-toluenesulfonate; the alkylsulfonic acid being selected from the group consisting of methanesulfonic acid, ethanesulfonic acid, propanesulfonic acid and trifluoromethanesulfonic acid; the arylsulfonic acid being selected from the group consisting of phenylsulfonic acid, phenolsulfonic acid and toluenesulfonic acid; the chloride ion source being selected from the group consisting of copper chloride, tin chloride and hydrochloric acid; the concentration of the halide ions of the halide ion source being 50-100 ppm; and the concentration of the leveling agent being 5-10 ppm.
 6. The metal electroplating composition according to claim 1, wherein the raw material of the metal electroplating composition comprises at least one of an accelerator and an inhibitor.
 7. The metal electroplating composition according to claim 6, wherein when the raw material of the metal electroplating composite comprises the accelerator, a concentration of the accelerator is 0.1 to 1000 ppm and the accelerator is selected from the group consisting of N,N-dimethyl-disulfenylcarbamic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonic acid-(3-sulfopropyl) ester, 3-mercapto-propylsulfonate sodium salt; disulfenyl carbonate-o-ethyl ester-s-ester and 3-mercapto-1-propane sultanate potassium salt, disulfopropyl disulfide, 3-(benzothiazolyl-s-sulfenyl)propyl sultanate sodium salt, pyridinium propyl sulfonyl betaine, 1-sodium-3-mercapto propane-1-sulfonate, N,N-dimethyl-disulfenyl carbamic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl propyl sulfonic acid-(3-sulfoethyl) ester, 3-mercapto-ethyl sultanate sodium salt, carbonic acid-disulfenyl-o-ethyl ester-s-ester and 3-mercapto-1-ethanesulfonate potassium salt, disulfoethyl disulfide, 3-(benzothiazolyl-s-sulfenyl)ethyl sultanate sodium salt, pyridinium ethyl sulfonyl betaine and 1-sodium-3-mercaptoethane-1-sulfonate; and wherein when the raw material of the metal electroplating composition comprises the inhibitor, a concentration of the inhibitor is 1 to 10000 ppm and the inhibitor is selected from the group consisting of polypropylene glycol copolymer, polyethylene glycol copolymer, ethylene oxide-propylene oxide copolymer, and butanol-ethylene oxide-propylene oxide copolymer.
 8. The metal electroplating composition according to claim 7, wherein when the raw material of the metal electroplating composition comprises the inhibitor, the inhibitor is a butanol-ethylene oxide-propylene oxide copolymer having a weight-average molecular weight of 100-100,000; and the concentration of the inhibitor is 5-10000 ppm.
 9. The metal electroplating composition of claim 6, wherein the raw material of the metal electroplating composition consists of the metal electroplating liquid, the leveling agent, the accelerator and the inhibitor.
 10. A method for electroplating a substrate, which comprises: (1) contacting the substrate to be electroplated with the metal electroplating composition according to claim 1; (2) applying an electric current for electroplating.
 11. The method according to claim 10, wherein the method includes at least one selected from the group consisting of: in step (1), the substrate is a wafer or chip of a printed circuit board or an integrated circuit; in step (2), the current density of the electroplating is 0.1-10 ASD; in step (2), the electroplating time is 53-110 s; in step (2), the electroplating temperature is 10-65° C.
 12. The method according to claim 10, wherein step (2) is carried out in three steps: in a first step, the current density is 0.1-0.5 ASD; the electroplating time is 3-20 s; and the electroplating temperature is 10-65° C.; in a second step, the current density is 0.5-1.5 ASD; the electroplating time is 20-30 s; and the electroplating temperature is 10-65° C.; in a third step, the current density is 1-10 ASD; the electroplating time is 30-60 s; and the electroplating temperature is 10-65° C.
 13. The method according to claim 11, wherein, the method includes at least one selected from the group consisting of: in step (2), the current density of the electroplating is 0.3-5 ASD; in step (2), the electroplating time is 80-110 s; in step (2), the electroplating temperature is 10-35° C.
 14. The method according to claim 13, wherein, the method includes at least one selected from the group consisting of: in step (2), the current density of the electroplating is 0.5-1.5 ASD; in step (2), the electroplating temperature is 20-30° C. 